Process for the preparation of lactose-free and reduced phosphorus skim milk

ABSTRACT

A method of preparing a low calorie, Lactose-free and Phosphorus-reduced milk with multiple filtration, centrifugation, carbonation and phase separation steps to remove Lactose and Phosphorus from milk including skim milk. The method includes a filtration apparatus to employ ultrafiltration to remove Lactose and any component of Lactose. Ultra-Centrifugation is used additionally to increase and complete the removal of Lactose and to facilitate the reduction of Phosphorous in the final milk preparation. The process eliminates the conventional use of lactase enzyme to hydrolyze Lactose into its simple sugar components.

CROSS-REFERENCE TO RELATED APPLICATIONS

This regular utility application claims the benefit of U.S. ProvisionalApplication Ser. No. 62/493,422, filed Jul. 2, 2016, the contents ofwhich are incorporated herein by reference.

FIELD OF THE DISCLOSURE

This disclosure relates to methods for preparing milk to remove specificmilk components. More particularly, the disclosure relates to methods toremove Lactose and a portion of the phosphorus content from skim milk.

BACKGROUND OF THE DISCLOSURE

Lactose-free milk has become increasingly popular as a large part of theworld population is Lactose Intolerant (humans unable to metabolizeLactose naturally present in milk). This problem is caused by theabsence of a digestive enzyme that breaks down Lactose, which is alsoknown as milk sugar. When a person who suffers from Lactose Intoleranceingests Lactose-laden products such as milk, the Lactose passesundigested into the lower gastrointestinal (GI) tract. Bacteriapopulations, naturally resident in the lower GI tract, digest theLactose and produce gas as a byproduct of the digestion. The gasproduction causes bloating and painful cramping in the host individual.

To address this issue, manufacturers chemically alter Lactose with anenzyme, lactase, that chemically cleaves the disaccharide Lactose sugarinto its two constituent simple sugars or monosaccharides, Glucose andGalactose. These simple sugars do not require additional processing asthe intestinal tracks of Lactose-intolerant individuals can absorb themonosaccharides directly into the bloodstream. These monosaccharidesmake milk taste sweeter as the monosaccharides bind differently tosweetness receptors on tongues. Although sweeter tasting, Lactose-freemilk contains the same calories as Lactose-laden milk since themonosaccharides remain in the milk. Moreover, use of lactase requires anadditional twenty hours of incubation to complete the hydrolysis processat 40° F. Manufacturers have tried to address these issue with purelymechanical means and with a modified combination of mechanical andchemical means to produce low-calorie, Lactose-free milk products.

With respect to a purely mechanical means of removing Lactose,filtration has been used to separate Lactose from other milk components.Lactose-free skim milk prepared by Ultra-Filtration (UF) alone has longbeen popular with manufacturers of reduced-carbohydrate foods andbeverages as a versatile ingredient that can offer more protein, calciumand potassium without Lactose. To create UF skim milk, processors passskim milk through a membrane that separates components by molecularsize. Smaller molecules, e.g., Lactose, soluble minerals and water, passthrough the membrane while larger molecules, e.g., casein and wheyproteins, are retained. It is this retained material that constitutes UFskim milk. Unfortunately, apart from removing Lactose, this process alsoremoves some important milk components beneficial to human health. TheseLactose-reduced products often are fortified with minerals and vitaminsto replace the removed nutrients. By removing Lactose with filtration,the calories associated with Lactose also are removed. Milk and milkproducts produced in this manner are lower in calories, but are not assweet as unfiltered milk. The filtration process, however, is imperfectand does not remove all the Lactose, which does not solve the problemfaced by Lactose-intolerant individuals that consume milk.

To eliminate any Lactose remaining in the UF milk after the UFfiltration process, a chemical process is applied after the mechanicalfiltration process. The remaining Lactose is hydrolyzed with the lactaseenzyme into the previously described monosaccharides. The need for anenzyme to breakdown the Lactose adds a significant cost and previouslynoted time component to the production of Lactose-free milk. Inaddition, because the monosaccharides remain in the finished milk-basedproduct, the calories associated with Lactose via the simple sugarcomponents of Lactose also remain. This means that the conventionalmethods used to eliminate Lactose during Lactose-free milk production donot eliminate the calories associated with Lactose.

Ultra-filtered (UF) milk, processed using conventional methods, is usedto produce popular new dairy-based products and dairy-based foods andbeverages that are higher in protein, calcium, potassium, and lower incarbohydrates. Notably, there are low-calorie versions of Lactose-freemilk, but these products involve the removal of other high caloriccomponents of whole milk other than Lactose, or its monosaccharidecomponents. As explained, in conventional UF milk, the Lactose ispartially filtered out and any remaining Lactose is reduced to its twosimple sugar components with lactase and not removed from the finalproduct. Currently, low-calorie, Lactose-free skim milk used for theseproducts must be imported into the Western Hemisphere from Spain,Finland or India as there are no current commercial producers for thismilk product in the Western Hemisphere. What is needed and what we havecreated is a low-cost, enzyme-free process to eliminate Lactose in milkand the calories in milk derived from Lactose.

Another problem associated with skim milk products and milk products ingeneral is the presence of phosphorus. For individuals with compromisedhealth, and compromised kidneys in particular, the presence ofphosphorus in beverage and food products can be life threatening whenthe kidneys are not able to filter out and remove the phosphorus.Currently, there are no Phosphorus-reduced milk products commerciallyavailable anywhere in the world. What is needed and what we have createdis a second process that may be used alone, or in combination with theLactose removal process, to significantly reduce the presence ofphosphorus in milk. Milk, when properly prepared and processed inaccordance with the disclosure herein, is advantageous for specialconsumption by individuals suffering from advanced kidney disease thatrequire lower phosphorus content in consumed milk products.

Collectively, what is needed and what we have developed are relativelylow-cost Lactose and phosphorus removal processes that eliminate theneed to hydrolyze Lactose and that produce collectively a verylow-calorie, skim milk digestible by Lactose-intolerant individualsand/or by those unable to metabolize phosphorus. Separately, eachprocess can be used to produce either low calorie, Lactose-free skimmilk, or skim milk with low phosphorous content. These and other objectsof the disclosure will become apparent from consideration of thefollowing summary and detailed description sections of the disclosure.

SUMMARY OF THE DISCLOSURE

In one aspect of the disclosure, a batch of raw milk is separated at alowered, above-freezing temperature to separate the fat component fromthe protein and carbohydrate components, which together form skim milk.The skim milk is next pasteurized to eliminate the presence of anybacteria or other pathogens. Following pasteurization, the pasteurizedskim milk may be stored at a reduced temperature for further processingfor up to 72 hours, or may be immediately subjected to furtherprocessing with Ultra-Filtration (UF) and Ultra-Centrifugation (UC) withthe skim milk cooled to about 15° C. If to bused in Ultra-Filtration,the pasteurized skim milk is passed through a pre-filter to remove anylarge solids, or to prevent conglomerated particles from forming.

The UF unit is constructed from material suitable for product contactsuch as 304 stainless steel or better. Its product contact tubing finishis 32 Ra maximum and its tank sheet metal finish is 2B. All processconnections are made with tri-clamps. In an illustrative embodiment, thespecialized UF filtration unit is designed to operate in a continuousmode and is based upon up to about 20 hours of operation producingproduct and then about 4 hours of a clean in place (CIP) sanitationprocess per day.

The feed material is introduced into the unit on a continuous basis withthe concentrate and the permeate drawn off continually throughout theproduction run at a pre-set concentration level. The pre-setconcentration level may be set within a designated range. CIPcapabilities are built integrally to the system with provisions forcirculation of a cleaning agent followed by a sanitary water rinse.

The mass balance of feed material may involve the following contentparameters. For skim milk as the feed material, the following componentconcentrations may be present:

FEED PERMEATE CONCENTRATE True Protein % 3.18 0.01 6.03 NPN % 0.16 0.140.17 Lactose Content % 4.78 4.80 4.76 Acid % 0.10 0.10 0.10 Ash % 0.720.45 0.96 Fat % 0.06 0.00 0.11 Concentrate Ration 1.9X T.S. % 9.0 5.5012.14 Feed Rate 5.43 gpm Concentrate Rate 2.83 gpm Permeate Rate 2.60gpm

The filtration unit used in at least one embodiment of the disclosuremay have the following properties:

Number of Stages One Total Number of Membrane Elements Three TotalMembrane Area 58 M2 Membrane Model 6338 Spiral Wound Membrane TypePolyether Sulfone (PES) ATD Type Stainless Steel

The skim milk is then further separated quantitatively into a solidphase (Casein micelles, Fat Globules, Globular Proteins) and a liquidphase (containing dissolved sugars, minerals and lipoprotein particles)by Ultra-Centrifugation. Finally, the liquid phase of the milk is pumpedinto a multiphase UF unit. The solid phase of the skim milk may bepooled quantitatively at 7° C. until the UF-UC procedure is complete. Asused herein, Ultra Centrifugation shall mean exposing the skim milk to acentrifugal force equal to, or exceeding, about 20,000 rpm.

The solid phase isolated with Ultra-Centrifugation is collectedquantitatively in a jacketed stainless-steel tank equipped with a lowvortex agitator to reduce frothing during mixing. The collected solidphase is slowly agitated continuously to prevent sedimentation. Theprocess continues with processing steps performed on the liquid phase.

The liquid phase is quantitatively pumped into the Ultra-filtrationsystem which meets 3A sanitary dairy standards and contains thefollowing conventional operative elements: pumps, motors, flowtransmitters, temperature transmitters, pressure transmitters, proximityswitches, pressure gauges, process valves, a process control valve,sample valves, check valves, steam valves, steam traps, and a coolingmedia control valve. All of these components are used to preciselycontrol the disclosed processing steps.

The liquid phase, isolated via Ultra-Centrifugation, is furthersubjected to CO₂ bubbled into the liquid to drop the pH of the liquid.In one aspect of the disclosure, the pH level is maintained from about3.2 pH to about 6.5 pH, or from about 4.5 pH to about 5 pH. Thecarbonated liquid is maintained at a temperature of about 5° C. to causethe remaining Lactose to crystalize out of solution. The remainingLactose is removed with an additional filter step through a 40-micronfilter. The finished liquid phase is now added back quantitatively tothe preserved solid phase with milk agitation to reconstituteLactose-free skim milk. The resulting skim milk also may be spray driedand stored in powder form.

In another aspect of the disclosure the low calorie, Lactose-free skimmilk prepared in accordance with the Lactose removal process disclosedherein is now brought to about 65° F. with CO₂ gas added to the liquidphase. This procedure is continued until the pH of the liquid phasedrops to between about 4.5 and about 4.6. The process is continued untilthe casein of the milk coagulates. The coagulated milk is passed againthrough a filter to remove the coagulant as the retentate and allow theserum to pass through as the permeate. The coagulated retentate isretained. Calcium chloride is now added to the serum permeate.

The pH of the milk serum is adjusted to from about 6.5 to about 7.0 bythe addition of a base such as sodium hydroxide (NaOH). A whitecrystalline precipitate of calcium phosphate is formed and removed bypassing the milk serum through UF to retain the calcium phosphateprecipitate as retentate and allow the Phosphorus-reduced serum to passas permeate. The Phosphorus-reduced serum is now re-mixed with thereserved casein quantitatively to form a low-calorie, Lactose-free andlow-phosphorus skim milk. These and other aspects of the disclosure willbecome apparent from a review of the appended drawings and a reading ofthe following detailed description of the disclosure.

DETAILED DESCRIPTION OF THE DISCLOSURE

In one aspect of the disclosure, Bovine somatotropin (rBST) hormone-freeraw milk in a 2,710-kg batch is separated into skim milk and cream atabout 4° C. The cream is pooled in a stainless steel jacketed tank andchilled to about 7° C. and may be used to make butter, ice cream orother dairy products. The separation step may take place at atemperature from about 5° C. to about 7° C. The skim milk component isthen pasteurized at a temperature of approximately 72° C. for about 16seconds. The pasteurization temperature can vary about +/−2° C. Thepasteurized skim milk is then re-cooled to about 4° C. if it is to bestored prior to processing. The skim milk may be stored for a maximum ofabout 72 hours before processing with Ultra-Filtration (UF) andUltra-Centrifugation (UC). If the pasteurized milk is to be processedimmediately, the milk is pre-cooled to about 7° C. before proceeding.The temperature for this processing step can vary about +/−2° C., orfrom about 5° C. to about 9° C.

The pasteurized skim milk should be free of any additives and suspendedsolids. To eliminate the presence of any suspended solids, the milkshould be pre-filtered with a filter having pore sizes from about 30microns to about 40 microns to produce a skim milk product with thefollowing properties and specifications:

TOTAL PLATE COUNT maximum 20,000/ml SEDIMENT TEST maximum 0.5 mg pHbetween 6.6-6.8 TITRATABLE ACIDITY maximum 0.15% as lactic acid FATCONTENT maximum 0.5% by Mojonnier ENTRAPED AIR maximum 0.5% by volume

The pre-filtered, pasteurized skim milk is now cooled down toapproximately 4° C. with constant agitation in preparation for the nextprocessing step. Once the skim milk is cooled to the desiredtemperature, the skim milk is further processed withUltra-Centrifugation (UC) to separate the milk into solid and liquidphases. The solid phase is collected quantitatively and stored in ajacketed stainless-steel tank equipped with an agitator to agitate themilk to maintain the solids in a suspension. This phase of the milkincludes Casein micelles, Fat Globules and Globular Proteins.

Next, the separated liquid phase (containing water, dissolved sugars,minerals and lipoprotein particles) is pumped into the previouslydescribed Ultra-Filtration unit (UF). The unit includes a feed sectiondimensioned and structured to provide adequate flow and pressure to theUF unit during both production and CIP. To that end, the Feed Sectionparameters are as follows:

Feed material: Skim Milk

Feed Rate (Liters/Hr.): about 1,140 (5.0 gpm)

Feed Solids: (% TS): about 9.08

Feed Protein %: about 3.21 (about 37.1% protein/total solids)

Feed Lactose %: about 4.82

Feed Ash %: about 0.73

Feed NPN %: about 0.16

Feed Fat %: about 0.06

Concentration Ratio: about 2.2×

Concentrate Solids (% TS): about 13.26 (about 54.5% protein/totalsolids)

Operating Temperature: about 10° C.

Operating Pressure: about 40 psig

Mode of Operation: Continuous

These are optimum conditions set to assure maximum yield and minimalclogging of the filter membranes. It should be understood that theparameters, e.g., feed rate, can be altered from the optimum conditionsto produce milk products that remain within the scope and spirit of thedisclosure.

The feed section of the unit consists of conventional operativeelements, commonly known by those having ordinary skill in the art,including a Flow Divert Plate, Proximity Switch, Pneumatically ActivatedSanitary Valves, CIP Water Butterfly Valve with Positioner, a CheckValve, a Sample Valve, a Feed Balance Tank which may have a capacity offrom about 10 to about 25 gallons, a set of Feed Pumps to provideadequate feed flow at desired pressure during production and CIP, a CIPShell and Tube Heat Exchanger, a Feed Tank Level Transmitter, Feed FlowMeter, Pressure Transmitter, Temperature Transmitter, Pressure Gaugesand a Security Screen with ¼″ holes designed to prevent foreign materialfrom entering into the system. It should be understood that theconventional components of the processing apparatuses used to performthe processes disclosed herein do not form an integral part of theprocesses as different apparatus configurations may be used to performthe disclosed processes. It further should be understood that anydisclosed apparatuses used to perform the disclosed processes do notlimit the scope of the disclosed processes.

After passing through the Feed Section of the unit, the liquid phasepasses into the Ultra-Filtration stage that contains a re-circulationpump to provide a constant cross flow condition over the enclosed filtermembranes to optimize flux and minimize fouling. The UF stage alsocontains a shell and tube heat exchanger and a temperature transmitter.The filters used for the UF unit may be constructed in a form selectedfrom the group consisting of filter membranes, filter media, hollowfibers, tubular membranes, spiral wound and combinations thereof. Asused herein, “filter material” and/or “filtration material” shall meanany filter membrane, filter media, or any other material or substanceused to filter fluids including liquids and gases.

Filtration materials may be constructed from hydrophilizedpolyethersulfone (PES), nylon, cellulose acetate, cellulose nitrate,hydrophilized polyvinylidene (PVDF), polycarbonate, as well as otherswell known in the art. As an illustrative embodiment, the filters usedare hydrophilic spiral wound with pore sizes ranging from about 0.5microns to about 40 microns. Multiple layers may be used, each withdifferent pore sizes and even different porosities.

The UF stage filters the pasteurized liquid portion of the skim milk toremove Lactose and a small amount of minerals (i.e. calcium, phosphorusand water) to form a filtered liquid phase. After leaving the UF stage,the filtered liquid phase passes into the concentrate section whichremoves and directs any concentrates to either the downstream processingdrain or to a return path back to the feed balance tank forrecycling/filtering. This section consists of Pneumatically ActivatedSanitary Valves, a Concentrate Flow Control Valve, a Sample Valve, aconcentrate Flow Meter, Pressure Transmitters and a Concentrate TransferPump that collectively provide a means of transferring concentrate tofurther downstream processing. After leaving the concentrate section,the filtered liquid phase component now enters a permeate section of theUF unit.

In this section, the filtered liquid phase or permeate is directed toone of at least three possible paths. The first path directs thepermeate further downstream for additional processing. The second patheliminates the permeate via a drain. The third path sends the permeateback to the Balance Tank for recycling. The permeate section includesPneumatically Actuated Sanitary Valves, Sample Valves and a permeatetransfer pump which provides a means of transferring any permeate tofurther downstream processing, a permeate flow meter and a pressuretransmitter.

After leaving the UF system, food-grade Carbon Dioxide (CO₂) is bubbledthrough the filtered liquid phase to reduce the pH from about 4.5 toabout 5.0. The CO₂ infused filtered liquid phase is permitted to standat a constant 4° C. for approximately 6-10 hours. The hold temperaturecan vary from about 3° C. to about 7° C. At the end of the 6-10-hourperiod, the CO₂ infused filtered liquid phase is again passed throughthe pre-filter to remove any crystals of Lactose that may have formed toproduce a Lactose-free CO₂ infused filtered liquid phase. Through themulti-stage filtering, centrifugation and re-cycling process, up to thispoint in the process, approximately 100% of the resident Lactose isremoved from the liquid. Any milk sugars remaining in the liquid isnaturally occurring and not derived from Lactose. For example, themonosaccharides that comprise Lactose, Glucose and Galactose, may bepresent naturally in their monosaccharide form in very low percentagesper volume of liquid.

The solid and CO₂ infused filtered liquid phases are now recombined toform filtered Lactose-free skim milk in the stainless steel jacketedtank with no sheer agitation to assure thorough mixing. This process ismaintained at about 4° C. by flowing glycol or other cooling agentthrough the jacket of the tank. The set tank temperature can fluctuatefrom about 1° C. to about 7° C. and still maintain the filtered skimmilk product in an acceptable potable condition.

The process disclosed herein isolates Lactose from the other milkcomponents. The Lactose by-product obtained from the UF process ispooled in a separate holding tank and may be purified and sold as apurified Lactose ingredient to bakers, animal food manufacturers and thepharmaceutical industry. The re-combined solid and liquid phases may bebottled and pasteurized in the final processed form to render alow-calorie, Lactose-free milk product. The final product, produced withthe processes disclosed herein, represents the first low-calorie,Lactose-free grade A milk, flavored or unflavored, whole or skim,produced anywhere in the Western Hemisphere and the only Lactose-freeproduct produced without Lactose hydrolyzation. The final product may beincorporated into a variety of beverages, including straightlow-calorie, Lactose-free skim milk, and/or be used as a liquidingredient for various low caloric, Lactose-free milk-based beverages.

The final product may also be spray dried at low heat to produce alow-calorie, Lactose-free skim milk powder useful in the commercialbaking or pharmaceutical industries. It is expected that yields of 100%of removed Lactose are possible with the disclosed Lactose-removalprocess. Unlike prior processes that use enzymatic hydrolysis of theLactose molecule to remove Lactose, the process disclosed herein removesthe entire concentration of the Lactose disaccharide and does not leaveany monosaccharides, glucose and Galactose, in the final product. Due tothe complete removal of Lactose, all the calories associated with theLactose disaccharide are eliminated from the final product. Moreover,the relatively long, twenty-hour incubation period needed to completelactose hydrolysis is eliminated with this process.

In another aspect of the disclosure, the low calorie, Lactose-free skimmilk, prepared in accordance with the Lactose removal process disclosedherein, is now brought to about 65° F. with mild agitation in a jacketedstainless-steel tank with CO₂ gas added to the liquid phase through asparger as it recirculates back into the tank. This procedure iscontinued until the pH of the liquid phase drops to between about 4.5and about 4.6. The process is continued until the casein of the milkcoagulates. The coagulated skim milk is passed again through a 40-micronfilter to remove the coagulant as the retentate and allow the serum topass through as the permeate. The coagulated retentate is retained.Calcium chloride is now added to the serum permeate in an amount toprovide about 3-4 moles of calcium for every 2 moles of phosphorus inthe milk. (Milk serum contains about 0.3-0.7% protein and about0.063-0.071% phosphorus).

The pH of the milk serum is adjusted to from about 6.5 to about 7.0 bythe addition of a base such as sodium hydroxide (NaOH). A whitecrystalline precipitate of calcium phosphate is formed and removed bypassing the milk serum through UF as disclosed herein to retain thecalcium phosphate precipitate as retentate and allow thePhosphorus-reduced serum to pass as permeate. The Phosphorus-reducedserum is now re-mixed with the reserved casein quantitatively to form alow-calorie, Lactose-free and low-phosphorus skim milk. The compositionof the Lactose-free, low-phosphorus skim milk compares to standard skimmilk as follows:

MILK COMPARISON Per 8 oz. Serving Low Calorie, Lactose Free PhosphorusReduced Standard Skim Milk Skim Milk Protein 14.0 g 8.26 g Calcium 326mg 306 mg Magnesium 32 mg 27 mg Phosphorus 49.4 mg 247 mg Lactose <5.0 g12.47 g Potassium 389 mg 382 mg Carbohydrate <5.0 g 12.15 g Sugar <1.0 g12.0 g

To maintain the desired level of Calcium in the skim milk, additionalCalcium may be added to the mixture in the form of Calcium Gluconate orCalcium Citrate in a final amount of from about 4.8 to about 5.3gm/gallon of skim milk. The final product has elevated concentrations ofprotein, essentially no Lactose and the calories associated withLactose, and low levels of phosphorus that amount to less than 80% ofthe phosphorus levels found in conventional milk products such as wholemilk and skim milk. Because a significant portion of the milk solidshave been removed, e.g. cream and Lactose, the concentration of theremaining protein based component of the skim milk is higher per unitvolume of milk. Rather than 8 grams of protein per pint, the finalproduct has 14 grams of protein per pint.

While the present disclosure has been described in connection withseveral embodiments thereof, it will be apparent to those skilled in theart that many changes and modifications may be made without departingfrom the true spirit and scope of the present disclosure. By way ofillustration and not limitation, the starting material for thephosphorus removal process can be whole milk or skim milk that has notundergone the Lactose removal process disclosed herein. Accordingly, itis intended by the appended claims to cover all such changes andmodifications as come within the true spirit and scope of thedisclosure.

What I claim as new and desire to secure by United States Letters Patentis: 1-9. (canceled)
 10. A method of preparing Phosphorus-reduced skimmilk comprising the steps of: providing skim milk; heating or coolingthe skim milk to about 65° F.; bubbling CO₂ gas into the skim milk untila pH of from about 4.5 to about 4.6 is reached; coagulating a caseincomponent in the skim milk to form coagulated skim milk; filtering thecoagulated skim milk by passing it through a filter having pores,wherein each pore has a size of about 40 microns to separate thecoagulated casein as retentate and liquid serum as permeate; retainingthe coagulated casein as coagulated retentate; adding calcium chlorideto the permeate; adjusting the pH of the permeate to from about 6.5 toabout 7.0 with a base such as sodium hydroxide to form a whitecrystalline precipitate of calcium phosphate in the permeate; filteringthe permeate in an Ultra-Filtration unit to separate the calciumphosphate from the permeate to form a Phosphorus-reduced serum; and,mixing the coagulated retentate with the Phosphorus-reduced serum toform Phosphorus-reduced skim milk.
 11. The method of claim 10 furthercomprising the initial steps of: providing raw milk comprising skim milkand cream; separating the skim milk and the cream by lowering thetemperature of the raw milk to between about 2° C. and about 7° C.; and,removing the cream.
 12. The method of claim 10 wherein calcium chlorideis added in an amount of about 3 to about 4 moles of calcium for every 2moles of phosphorus in the skim milk.
 13. The method of claim 10 furthercomprising the step of adding Calcium to the Phosphorus-reduced skimmilk in the form of Calcium Gluconate or Calcium Citrate.
 14. The methodof claim 13 wherein the Calcium is added to achieve a final Calciumconcentration of about 4.8 to about 5.3 grams per gallon of skim milk.15. A method of preparing Lactose-free and Phosphorus-reduced milkcomprising the steps of: providing skim milk; pasteurizing the skimmilk; pre-cooling the skim milk to between about 5° C. to about 9° C.;pre-filtering the skim milk with a filter having pore sizes from about30 to about 40 microns to remove any suspended solids to formpre-filtered, pasteurized skim milk; cooling the pre-filtered,pasteurized skim milk to about 4° C.; separating solid and liquid phasesof the pre-filtered, pasteurized skim milk with Ultra-Centrifugation toproduce a solid phase comprising Casein Micelles, Fat Globules andGlobular Proteins and a liquid phase comprising water, dissolved sugars,minerals and lipoprotein particles; collecting and storing the solidphase in a stainless-steel tank; pumping the liquid phase into a feedsection of an Ultra-Filtration unit; filtering the liquid phase bypassing it through a filter secured in the Ultra-Filtration unit,wherein the filter has a plurality of pores having pore sizes rangingfrom about 0.5 microns to about 40 microns, and wherein a portion ofLactose and a portion of minerals present in the liquid phase arefiltered out to form a filtered liquid phase; cooling the filteredliquid phase to between about 5° C. and 7° C.; bubbling CO₂ into thefiltered liquid phase to reduce the pH to from about 4.5 to about 5.0 tocause any Lactose present to form into Lactose crystals and to form aCO₂ infused filtered liquid phase; returning the CO₂ infused filteredliquid phase to the pre-filter; passing the CO₂ infused filtered liquidphase through the pre-filter to remove any Lactose crystals present toform a lactose-free, CO₂ infused filtered liquid phase; recombining thesolid phase with the lactose-free, CO₂ infused filtered liquid phase inthe stainless-steel tank to form Lactose-free skim milk; heating orcooling the Lactose-free skim milk to about 65° F.; bubbling CO₂ gasinto the Lactose-free skim milk until a pH of from about 4.5 to about4.6 is reached; coagulating a casein component in the Lactose-free skimmilk to form coagulated skim milk; filtering the coagulated skim milk bypassing it through a filter having pores, wherein each pore has a sizeof about 40 microns to separate the coagulated casein as retentate andliquid serum as permeate; adding calcium chloride to the permeate;adjusting the pH of the permeate to from about 6.5 to about 7.0 with abase such as sodium hydroxide to form a white crystalline precipitate ofcalcium phosphate in the permeate; filtering the permeate in anUltra-Filtration unit to separate the calcium phosphate from thepermeate to form a Phosphorus-reduced serum; and, mixing the caseinretentate with the Phosphorus-reduced serum to form Lactose-free,Phosphorus-reduced skim milk.
 16. The method of claim 15 comprising theinitial steps of: providing raw milk comprising skim milk and cream;separating the skim milk and the cream by lowering the temperature ofthe raw milk to between about 2° C. and about 7° C.; and, removing thecream.
 17. The method of claim 16 further comprising the steps of:pooling the cream in a jacketed stainless-steel tank; and, chilling theseparated cream to about 7° C.
 18. The method of claim 15 furthercomprising the step storing the pasteurized skim milk at a temperatureof about 4° C. before the pre-cooling step.
 19. The method of claim 15further comprising agitating the pre-filtered, pasteurized skim milkwhile cooling it down before the Ultra-Centrifugation step.
 20. Themethod of claim 15 further comprising the step of agitating the solidphase when collecting and storing the solid phase in a jacketedstainless-steel tank to maintain solids in suspension.
 21. The method ofclaim 15 further comprising the step of passing the filtered liquidphase into a concentrate section of the Ultra-Filtration unit to removeand direct concentrates to a path selected from the group consisting ofa downstream path for further processing, a drain path for elimination,a recycling path and combinations thereof.
 22. The method of claim 15further comprising the step of permitting the CO₂ infused liquid phaseto stand for approximately 6-10 hours before recycling the CO₂ infusedliquid phase through the pre-filter.
 23. The method of claim 15 furthercomprising the step of spray drying the Lactose-free, Phosphorus-reducedskim milk to product Lactose-free, Phosphorus-reduced skim milk powder.24. The method of claim 15 wherein calcium chloride is added in anamount of about 3 to about 4 moles of calcium for every 2 moles ofphosphorus in the skim milk.
 25. The method of claim 15 furthercomprising the step of adding Calcium to the Phosphorus-reduced skimmilk in the form of Calcium Gluconate or Calcium Citrate.
 26. The methodof claim 25 wherein the Calcium is added to achieve a final Calciumconcentration of about 4.8 to about 5.3 grams per gallon of skim milk.